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Regulatory Mechanisms
in Biosystems
Regulatory Mechanisms
in Biosystems
ISSN 2519-8521 (Print) ISSN 2520-2588 (Online) Regul. Mech. Biosyst., 9(3), 430-434 doi: 10.15421/021864
Optimization of the 9a-hydroxylation of steroid substrates using an original culture of Rhodococcus erythropolis
V. A. Andryushina, N. V. Karpova, T. S. Stytsenko, V. V. Yaderets, E. D. Voskresenskaya, V. V. Dzhavakhia
Federal Research Center "Fundamentals of Biotechnology", Russian Academy of Sciences, Moscow, Russian Federation
Article info
Received 07.06.2018 Received in revised form
12.07.2018 Accepted 16.07.2018
Federal Research Center "Fundamentals of Biotechnology", Russian Academy of Sciences, Leninskyprospect, 33/2, Moscow, 119071, Russian Federation. Tel.: +7-499-135-30-49. E-mail:
andryushina@rambler. ru
Andryushina, V. A, Karpova, N. V., Stytsenko, T. S., Yaderets, V. V., Voskresenskaya, E. D., & Dzhavakhia, V. V. (2018). Optimization of the 9a-hydroxylation of steroid substrates using an original culture of Rhodococcus erythropolis. Regulatory Mechanisms in Biosystems, 9(3), 430-434. doi:10.15421/021864
To obtain inoculation material (cultivation stage 1), the biomass of Rhodococcus erythropolis VKPM AC-1740 was transferred from agar slants into 750 ml conic flasks containing 100 ml of vegetation media of the following composition (g/l): medium 1 - yeast extract, 10.0; glucose, 10.0; soybean flour, 10.0; KH2PO4, 2.0; Na2HP04, 4.0 (pH 6.8-7.4); medium 2 - corn extract, 15.0; glucose, 10.0; KH2PO4, 2.0; Na2HP04, 4.0 (pH 6.8-7.4). The culture was grown on a rotary shaker (220 rpm) for 68-72 h at 28-29 °C. To obtain a working biomass (cultivation stage 2), the inoculum obtained at the stage 1 was transferred into flasks containing the same media (the volume of seed material was 20% of the medium volume) and grown under the same conditions for 23-25 h. During a study of the effect of the inducer concentration on the rate of 9a-OH-AD formation, different concentrations (0.25, 0.50, and 1 g/l) of the AD solution in dimethylformamide (DMF) were added to the vegetation medium after 6 h of incubation. To perform AD transformation at a load of 5 g/l, 10 ml of Rh. erythropolis cells at the age of 23-25 h were transferred into 750 mL flasks with baffles containing 40 mL of vegetation medium supplemented with the steroid. AD was added in the form of microcrystals or suspension with a surfactant or DMF. The process was carried out at 28-29 °C and with constant mixing (220 rpm). During AD transformation at a load of 10-30 g/l, the steroid was preliminarily precipitated from DMF solution. The resulting paste was mixed with a surfactant and transformation medium. The obtained homogeneous suspension was poured in equal amounts into the flasks with baffles, and then a concentrated cell mass was added (25 vol.%). To obtain a cell concentrate, cells were centrifuged for 1 h at 1500 rpm at the age of 23-25 h. The resulting biomass was homogenized, supplemented with a fresh medium to the required volume, and added into transformation flasks. The amount of a biomass required for AD transformation at a load of 10 g/l was 3.13 g/l (dry weight); in the case of a 30 g/l load, the biomass was added by two equal portions, and its total amount was 6.2 g/l (dry weight). The amount of 9a-OH-AD in a culture broth was evaluated by a thin-layer chromatography (TLC) and high-performance liquid chromatography (HPLC). Steroids were extracted by ethylacetate. To perform TLC, Sorbifil plates (Russia) and benzol: acetone mix (3 : 1) were used. HPLC was performed on a Gilson chromatographer (United States) equipped with a Silasorb C-18 column (10 ^m, 4.0 x 250 mm); the flow rate was 0.8 ml/min. The mobile phase was MeOH : H20 mix (70 : 30). The absorbance was measured at 260 nm. Replacement of corn extract, which has an unstable composition, by yeast extract and soybean flour and the use of glucose as an optimal carbon source for a Rh. erythropolis culture have provided a high-yield production of 9a-hydroxy-4-ene-3,17-dione with increased AD loads. Use of such techniques as the inoculum induction and application of surfactants have provided a positive effect on the AD transformation with a load exceeding 10 g/l. During 9a-hydroxylation of AD with a load of 30 g/l, a target product with the yield of 83% has been obtained.
Keywords: fluorinated corticoids; AD; 9a-OH-AD; Rhodococcus erythropolis VKPM AC-1740; surfactants; inducer.
Introduction
Deterioration of environmental conditions and the corresponding increase in the number of allergic and inflammatory diseases on the global scale gives rise to a growing need for steroid preparations of different therapeutic action. According to analytic forecasts, the volume of the steroid market in 2021 will reach 4.480 million US dollars (Fernandez-Cabezon et al., 2018; Barredo & Herraiz, 2017, Fernandes et al., 2003). Thus, despite the existing achievements in the biotechnology of steroid production, the development of effective methods of synthesis of androgenic, gestagenic, mineral, and glucocorticoid steroid preparations from natural plant products still remains relevant (Brzezinska et al., 2013; Guevara et al., 2017a; Fernandez-Cabezon et al., 2018).
The main indications for glucocorticosteroid therapy of humans include rheumatoid arthritis, bronchial asthma, neurodermatitis and other skin and allergic diseases, acute adrenal insufficiency, and also various shock states (post-rheumatic, operational, toxic, burn, etc.). Today the most
common anti-inflammatoiy steroids represent structural modifications of natural compounds and are characterized by improved therapeutic properties and weaker side effects. Among such preparations, fluorinated corticosteroids (dexamethasone, sinaflan, triamcinolone, fluticasone, etc.) are in the greatest demand (Mashkovskiy, 2012).
9a-hydroxy-4-ene-3,17-dione (9a-OH-AD) is the basic intermediate in the synthesis of the aforementioned drug preparations from sterols (Fernández de las Heras et al., 2012; Mohn et al., 2012; Jakociunas et al., 2016; Mondaca et al., 2017). According to the existing data, 9a-hydro-xylation, which represents a key reaction in the synthesis of fluorinated corticoids, cannot be realized via chemical synthesis (Guevara et al., 2017). Therefore, a cost-efficient large-scale production of this class of drugs is possible only with the use of microorganisms able to perform a highly selective targeted transformation of steroid molecules of a given structure under ecologically safe conditions and without any need for preliminary protection of the functional groups of the initial molecule (Mutafova et al., 2016; Smitha et al., 2017).
It is known that some lower fungi (Ascochyta, Helicostilum, Circi-nella) and many bacteria, especially actinobacteria (Arthrobacter, Cory-nebacterium, Mycobacterium, Nocardia, Rhodococcus) are able to introduce 9a-hydroxygroups into a steroid molecule. However, steroid hydroxylation with fungi does not provide a sufficient selectivity of the process. Along with the formation of a target hydroxysteroid, fungi also produce a number of side mono- and dihydroxy-products, which complicates the further isolation of the target product and significantly reduces its yield. In addition, both position and orientation of an introduced hydroxyl group strongly depends on the structure of the steroid molecule (Donova & Egorova, 2012; Andryushina et al., 2013; Barredo & Herraiz, 2017).
Unlike fungi, bacteria perform 9a-hydroxylation reaction regardless of the steroid structure and presence of additional bonds and substituents. Therefore, actinobacteria capable of providing a high-selective introduction of a hydroxy group at the 9a-position of a steroid molecule may be considered as the most promising bioreagents, since the corresponding bacterial enzyme shows the lower substrate specificity than steroid 9a-mo-nooxygenase of a fungal origin (Petrusma et al., 2009, 2011; Lee et al., 2016; Nielsen & Keasling, 2016). However, 9a-hydroxylation activity was detected only in bacteria which were able to use steroids as a carbon source since this reaction represents an intermediate stage of a complete cleavage of steroid molecules to CO2 and H2O, at which the simultaneous action of 3-ketosteroid-1,2-dehydrogenase and 9a-hydroxylase is observed (Petrusma et al., 2014; Donova & Egorova, 2012; Rodina et al., 2009). The analysis of published data showed that the selective 9a-hyd-roxylation without any destruction of a steroid nucleus can be performed using bacterial strains carrying mutations, which block the biosynthesis of 1,2-dehydrogenase or prevent the functioning of this enzyme. In our previous study, we obtained a highly-selective Rhodococcus erythropo-lis strain VKPM AC-1740 with improved 9a-hydroxylating activity (Rodina et al., 2009; Carpova-Rodina et al., 2011). Using this strain, we developed efficient technologies for the production of 9a-hydroxy-ste-roid derivatives (Vojshvillo et al., 2007) and developed several efficient methods for 9a-OH-AD production from sterols including the mixed culture method (Andryushina et al., 2011) or the use of original biocata-lyst representing R erythropolis VKPM AC-1740 cells immobilized in a PVA cryogel (Carpova-Rodina et al., 2011).
A common disadvantage of all methods for 9a-hydroxylation of steroids, which were previously developed by our team, was the dependence of the hydroxylating activity of R erythropolis VKPM AC-1740 on a nutrient medium composition, namely, the quality of the corn extract used as the main nitrogen source (Ribeiro et al., 2017; van der Geize et al., 2001, 2001, 2008). The composition of a corn extract is determined by several factors, such as the grain quality, scheme and mode of its soaking, and the extract thickening procedure. Corn extract may contain some impurities, which provide a negative effect on microorganisms and reduce their enzymatic activity. Because of fluctuations in the activity of a culture grown on such medium, there is a need to select an alternative nitrogen source with the further optimization of the hydroxylation process under new fermentation conditions. At this stage of our work, yeast extract was chosen as a stable and available source of organic nitrogen.
Thus, the aim of this study was to evaluate the 9a-hydroxylating activity of R erythropolis VKPM AC-1740, grown on media contain-ning yeast extract and soybean flour as the main nitrogen sources, in relation to the production of 9a-OH-AD from AD at the initial AD concentration equal to 10-30 g/l.
Materials and Methods
Strain, nutrient media and cultivation conditions. The earlier developed R erythropolis VKPM AC-1740 strain characterized by a high 9a-hydroxylating activity in relation to A4-3-ketosteroids, was used in the study. The culture was stored on solid agar medium of the following composition (g/l): yeast extract, 10.0; glucose, 10.0; KH2P04, 1.0 (pH 6.8-7.2). To obtain inoculation material (cultivation stage 1), the biomass of R erythropolis was transferred from agar slants into 750 ml conic flasks containing 100 ml of vegetation media of the following composition (g/l): medium 1 - yeast extract, 10.0; glucose, 10.0; soy-
bean flour, 10.0; KH2P04, 2.0; Na2HP04, 4.0 (pH 6.8-7.4); medium 2 -com extract, 15.0; glucose, 10.0; KH2P04, 2.0; Na2HP04, 4.0 (pH 6.87.4). The culture was grown on a rotary shaker (220 rpm) for 68-72 h at 28-29°C.
To obtain a working biomass (cultivation stage 2), the inoculum obtained at the stage 1 was transferred into flasks containing the same media (the volume of seed material was 20% of the medium volume) and grown under the same conditions for 23-25 h. During the study of the effect of the inducer concentration on the rate of 9a-OH-AD formation, different concentrations (0.25, 0.50, and 1 g/l) of the AD solution in dimethylformamide (DMF) were added to the vegetation medium after 6 h of incubation.
Biotransformation conditions. To perform AD transformation at a load of 5 g/l, 10 ml of R erythropolis cells at the age of 23-25 h were transferred into 750 ml flasks with baffles containing 40 ml of vegetation medium supplemented with the steroid. AD was added in the form of microcrystals or suspension with a surfactant or DMF. The process was carried out at 28-29 °C and a constant mixing (220 rpm).
During AD transformation at a load of 10-30 g/l, the steroid was preliminarily precipitated from the DMF solution. The resulting paste was mixed with a surfactant and transformation medium. The obtained homogeneous suspension was poured in equal amounts into the flasks with baffles, and then a concentrated cell mass was added (25 vol.%).
To obtain a cell concentrate, cells were centrifuged for 1 h at 1500 rpm at the age of23-25 h. The resulting biomass was homogenized, supplemented with a fresh medium to the required volume, and added into transformation flasks. The amount of a biomass required for AD transformation at a load of 10 g/l was 3.13 g/l (dry weight); in the case of a 30 g/l load, the biomass was added by two equal portions, and its total amount was 6.2 g/l (dry weight).
Transformation efficiency assessment. The amount of 9a-OH-AD in a culture broth was evaluated by a thin-layer chromatography (TLC) and high-performance liquid chromatography (HPLC). Steroids were extracted by ethylacetate. To perform TLC, Sorbifil plates (Russia) and benzol: acetone mix (3 : 1) were used. HPLC was performed on a Gilson chromatographer (United States) equipped with a Silasorb C-18 column (10 pm, 4.0 x 250 mm); the flow rate was 0.8 ml/min The mobile phase was MeOH : H20 mix (70 : 30). The absorbance was measured at 260 nm.
Results
Selection of Nitrogen and Carbon Sources. At the first stage of a nutrient medium optimization, a comparative 9a-hydroxylation of AD with a 5 g/l load was carried out using media 1 and 2. The obtained results were identical for both media: a complete conversion of the initial compound with the formation of 4.7-4.8 g/l of 9a-OH-AD occurred within 20-22 h. Replacement of a carbon source in the medium 1 provided a more significant impact on the AD biotransformation process (Table 1). According to the obtained data, the best result was obtained using a modified medium containing soybean flour, yeast extract, and glucose. After 21 h of the AD transformation (5 g/l load) in a modified medium, almost complete substrate conversion was observed with the formation of 9a-OH-AD as an individual compound. Therefore, this medium was chosen as the basic one for the further optimization ofthe conversion process.
Table 1
Effect of various carbon sources on the production of 9a-OH-AD by Rhodococcus erythropolis VKPM AC-1740
Carbon source Average steroid content in a culture broth, %
(5 g/L) 9a-OH-AD AD
Control (no carbon source) 68 ± 1.5 30 ± 1.5
Glucose 98 ± 1.0 2 ± 1.0
Fructose 15 ± 1.3 84 ± 1.3
Sucrose 40 ± 0.8 60 ± 0.8
Lactose 12 ± 1.5 85 ± 1.5
Note: hereinafter, the experimental error (±) was determined as a random error of direct measurements using the following formula: Ax = (xmax - xmj„)/2, where xmax h xmin are the maximum and minimum values obtained by the series of repeated measurements.
Effect of the AD introduction method on the 9a-0H-AD output. As we have mentioned earlier, one of the main problems of microbiological transformations of steroid substrates is the high hydrophobic property of steroid molecules; the solubility of steroids belonging to the androstane group does not exceed 20 mg/l (Goetschel & Bar, 1992). To solve this problem, we added AD into a medium either in the form of a fine-dispersed suspension with various surfactants, or dissolved in DMF (Table 2).
Table 2
Effect of various surfactants on the production of 9a-OH-AD
by Rhodococcus erythropolis VKPM AC-1740
Surfactant used for
Average steroid content
introduction of ground AD in a culture broth (TLC), %
into fermentation medium 9a-OH-AD AD
Tween 21* 97 ± 1.5 3 ± 1.5
Tween 40 96 ± 1.3 4 ± 1.3
Tween 61 96 ± 1.4 4 ± 1.4
Tween 80 99 ± 0.3 1 ± 0.3
Triton 100 95 ± 1.6 5 ± 1.6
Span 20 98 ± 1.3 2 ± 1.3
Span 80 97 ± 1.5 3 ± 1.5
Emulan EL 90 ± 1.3 10 ± 1.3
DMF** 95 ± 1.3 5 ± 1.3
Control 98 ± 0.5 2 ± 0.5
Note: * - surfactant : AD ratio is 1 : 4; ** - DMF 4 vol.%.
According to the obtained results, the most efficient AD transformation at a 5 g/l load was observed in the variant with Tween 80. However, the control variant (i.e., without addition of any surfactant or solvent) demonstrated a quite comparable result.
Effect of the Inducer on a Microbiological 9a-Hydroxylation by R. erythropolis VKPM AC-1740. 3-Ketosteroid-9a-hydroxylase (9-KSH) is a two-component non-heme iron-dependent Rieske monooxygenase consisting of a KshA oxygenase and a KshB reductase. 9-KSH is one of the key enzymes involved into a microbiological degradation of steroids and is of a great physiological importance for a wide range of steroid-transforming bacteria (Petrusma et al., 2014). The presence of a 3-keto group and also A1 and / or A4-double bonds in the A ring of the steroid nucleus is a necessary condition for a 9a-hydroxylase activity (Akhrem & Titov, 1970).
To study the stimulation of a 9-KSH biosynthesis, the inoculum of R. erythropolis VKPM AC-1740 was grown on a medium supplemented with AD as an inducer (0.25, 0.50, and 1.0 g/l). The AD solution was added 6-7 h after inoculation by a second-generation culture. The total time of incubation was 23-25 h. The amount of the inoculum used for transformation of AD (5 g/l) was 20% of the medium volume. The result of the experiment is shown in Table 3.
Table 3
Consumption of AD (5 g/l) and accumulation of 9a-OH-AD by R. erythropolis VKPM AC-1740 grown in the presence of various concentrations of the inducer
Average steroid content in a culture broth, %
Time,
control
inducer concentration, g/L
0.25
0.50
1.00
AD 9a-OH- AD 9a-OH- AD 9a-OH- Afl 9a-OH-
AD AD AD AD
0 5.0 - 5.0 - 5.0 - 5.0 -
2 5.0 - 4.9 0.1 4.8 0.1 4.7 0.2
4 5.0 - 4.7 0.2 4.6 0.2 4.5 0.3
6 4.8 0.1 4.4 0.3 4.4 0.3 4.3 0.4
12 1.9 2.9 1.5 3.2 1.3 3.4 1.2 3.3
14 1.4 3.5 0.9 3.1 0.9 3.3 0.8 3.0
16 1.0 3.9 0.4 3.0 0.3 3.1 0.2 2.9
18 0.6 4.3 - 2.5 - 2.6 - 2.5
20 0.1 4.7 - 2.1 - 2.4 - 2.0
The 9a-hydroxylating activity of R. erythropolis VKPM AC-1740 in the presence of the inducer was observed already after 2 h of transformation, whereas in the control variant it was registered only after 6 hours of transformation. For all variants with induced seed material, we observed an active destruction of the target product during transformation. A pro-
bable explanation is that the induction of a 9-KSH biosynthesis may result in the induction of 1,2-dehydrogenase, responsible for the next reaction in the steroid nucleus degradation pathway.
Results obtained in this experiment were used for the study of the AD transformation at a load of 10-30 g/l. AD transformation into 9a-OH-AD at a substrate load of 10 g/l. The effect of induction on the AD transformation at a load of 10 g/l was examined using a concentrated R. erythropolis VKPM AC-1740 biomass (3.13 g/l of dry weight). The transformation time was 19-20 h. The yield of 9a-OH-AD equal to 94.3% and 94.0% (as determined by HPLC) was obtained in the case of the inducer concentration equal to 0.5 g/l; this yield exceeded that of the control by 10% (Fig. 1). A slight destruction of the target product was observed at the inducer concentration equal to 1.0 g/l (Figs. 1, 2).
ill!
0.25 g/L
0.5 g/l
1.0 g/l
Fig. 1. Effect of various inducer concentrations on the yield of 9a-OH-AD at the end of the AD transformation by Rhodococcus erythropolis VKPM AC-1740: for all variants, the AD concentration was 10 g/l
Fig. 2. 9a-OH-AD crystals in a culture broth AD transformation into 9a-OH-AD at a substrate load of 30 g/l
The AD transformation at a load of 30 g/L was carried out under conditions selected in the previous experiments. To improve the biotrans-
formation process, an additional portion of a concentrated inoculum and a glucose solution (5 g/l) were added during the process (Fig. 3).
Fig. 3. Dynamics of 9a-OH-AD accumulation at the AD load of 30 g/l
According to this experiment, the substrate was completely transformed into 9a-hydroxyproduct within 44 h of incubation. The yield of a technical 9a-OH-AD substance reached 83%, while its content determined by HPLC was 93.6%.
Discussion
According to many authors, nutrient medium composition influences the direction of the steroid reaction and on the rates of consumption of the initial substrate and accumulation of the target product. For example, changes in the concentration or the origin of organic nitrogen in a nutrient medium directly affect the biomass accumulation rate and can change the hydroxylating activity of cells. It was shown that the use of non-dehydrated nitrogen sources, such as casein, gelatin, and meat extract, provided a biomass possessing the higher transformational activity (Angelova et al., 1995). Soybean flour contains fatty acids, which positively influence the permeability of a bacterial cell wall and improve the availability of lipophilic substrates, such as steroid compounds, for enzymes of steroid-transforming microorganisms. Soybean flour also contains lecithin, a natural emulsifier preventing aggregation of steroid particles.
The results obtained in our study revealed no correlation between the biotransformation ability of Rh. erythropolis VKPM AC-1740 and the nitrogen source. The effect of a carbon source on the yield of a target 9a-OH-AD was more significant. We showed that the absence of glucose (preferred carbon source) in the medium resulted in a decreased 9a-hydroxylation rate as compared with the glucose-containing medium (Table 1). We also observed the inhibition of a 9a-hydroxylase activity in the media containing lactose or fructose as a carbon source. Our results agree with the data obtained by Angelova et al. (1995), who also showed the maximum biomass accumulation and a high substrate conversion rate in a glucose-containing medium.
A high hydrophobic property of steroid substrates in aqueous media results in a low degree of conversion of the initial substrate and a low yield of the target reaction product. Traditional approaches to reducing mass transfer limitations include the use of a fine-grain substrate and various surfactants or solvents able to mix with water, such as dimethyl sulfoxide, DMF, methanol, acetone, and 1,2-propanediol. To prevent deactivation of the biocatalyst, the amount of the added solvent usually does not exceed 1.5-5.0%o (v/v) (Fernandes et al., 2003). In addition, it is known that solvents may provide different effects, such as changes in the rate and direction of hydroxylation, as well as the stimulation or suppression of the by-product formation. According to some authors, microorganisms can include some solvents into their metabolic pathways to regenerate reduced cofactors (Angelova et al., 1995). Avramova et al. (2010) showed that the presence of Tween 80 in a glucose-containing medium accelerated the process of the 9a-hydroxylation of AD.
In this study we showed that the surfactant presence in the nutrient medium during the AD transformation at a load within 5 g/l did not result in an expected increase in the 9a-OH-AD generation rate as com-
pared to the control (Table 2). A probable reason is that the strain itself may be able to emulsify and degrade hydrophobic substrates. According to the existing publications, such ability is determined mainly by specific structural features of the cell membrane of this microorganism, which is lipophilic, i.e., has a high affinity to hydrophobic substrates (Tsitko et al., 1999). The surface activity and hydrophobic character of the cell membrane promote interaction between the cells and insoluble substrate, which makes it possible to overcome a limited diffusion during the substrate uptake into a cell (Kostina, 2008). In addition, the composition of soybean flour includes lecithin, a natural emulsifier preventing aggregation of steroid particles (Petrusma et al., 2009; 2011; Jakociunas et al., 2016; Liu et al., 2016). It is known that A1-2-dehydrogenation and 9a-hydroxylation reactions resulting in the opening of the B ring of the steroid structure are the key reactions in the process of steroid utilization as carbon sources (Marques et al., 2010; Wilbrink et al., 2011; Brzezin-ska et al., 2013; Yeh et al., 2014). Data shown in Table 3 allow us to assume that the induction of the 9a-KSH synthesis resulted in the induction of 1,2-dehydrogenase, responsible for the next reaction in steroid nucleus degradation pathway. This hypothesis may provide an explanation of the observed active 9a-OH-AD destruction. A possible reason for the lack of any undesirable 9a-OH-AD degradation (which was observed at the AD load of 5 g/l) during the AD transformation at a load of 10 g/l is that the increased AD load resulted in the accumulation of 9a-OH-AD in the culture broth in the form of crystal-like structures (Fig. 3) unavailable for the further microbial destruction (Rodina et al., 2009). During this study we selected optimal conditions providing AD transformation at a load of 30 g/L and obtaining a high output of a technical product. Our results suggest that further work is needed on the nutrient medium optimization and study of the effect of optimized media on the 9a-KSH activity of R erythropolis VKPM AC-1740 to provide the further increase of the AD load and to obtain a high yield of 9a-OH-AD.
An obvious advantage of the proposed technology is acceleration of the transformation process due to a high substrate availability and use of a concentrated biomass that makes it possible to transform AD under high loads and under non-sterile conditions.
Conclusion
Replacement of corn extract with yeast extract and soybean flour, as well as the choice of glucose as a carbon source provided reduction of the duration of transformation while still maintaining a high 9a-OH-AD yield. At the same time, the effect of surfactants and the effect of 9-KSH-mediated induction of R erythropolis VKPM AC-1740 were positive only if they were applied for transformation with an increased substrate load. A 44-h AD transformation at a load of 30 g/l by R erythropolis VKPM AC-1740 resulted in the production of 9a-OH-AD with the yield of 83.0%; the content of the target compound determined by HPLC was 93.6%.
This study was supported by the programme of the Presidium of the Russian Academy of Sciences "Development of new biotechnological methods for obtaining highly active fluorinated corticosteroids of anti-inflammatory and antiallergic action from phytosterols via 9a-hydroxy-AD using biologically modified immobilized biocatalysts" (project 1201371077).
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